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62results about How to "Mild and controllable reaction" patented technology

Cationic waterborne polyurethane resin and preparation method thereof

The invention discloses cationic waterborne polyurethane and a preparation method thereof, and relates to the technical field of polyurethane. The problems that an existing cationic waterborne polyurethane preparation method is complex in technology, and prepared waterborne polyurethane emulsion cannot get rid of the dependency on petrochemical resources are solved. The structural formula of the cationic waterborne polyurethane is shown as a formula (1) (please see the formula in the description). The invention further provides a preparation method of cationic waterborne polyurethane resin. The preparation method comprises the steps that firstly, under protection of inert gas, poly(carbonic ester-ether)dihydric alcohol reacts with diisocyanate in organic solvent to obtain a first intermediate; secondly, the first intermediate reacts with a hydrophilic chain extender under action of a catalyst to obtain a second intermediate; lastly, the second intermediate reacts with butanediol, acid is added for neutralization, deionized water is added to remove the solvent through emulsifying and steaming, and then the cationic waterborne polyurethane resin is obtained. The polyurethane resin is excellent in performance, and waterborne polyurethane can reduce the dependency on the petrochemical resources.
Owner:中科应化(长春)科技有限公司

Gas phase SO3 film-scrapping sulfonating technology

The invention relates to a gas phase SO3 film-scraping sulfonating technology which belongs to the technical field of production technology which prepares anionic surfactant by using gas phase SO3 film-scraping sulfonating liquid organic materials. The invention is carried out according to the following steps: A: liquid SO3 is vaporized to gas phase SO3, the gas phase SO3 is sucked in a mixer shaft through a turbo-blower, the gas phase SO3 is mixed with inert gases recycled in a sulfonating reactor to reaction gas with the volume concentration being 0.1 to 10 percent, and then the reaction gas goes into a reaction cylinder body through reaction gas distribution holes on the upper part of the scraping plate shaft; B: the organic materials go into the sulfonating reactor and downwards flow along the inner wall of the reaction cylinder body, a scraping plate is rotated along with the mixer shaft under the action of a transmission system, the organic materials are continuously suffered with film scaping-spread coating-film scaping in the inner wall of the reaction cylinder body, the organic material are alternately updated and uniformly coated on the inner wall of the reaction cylinder body, and the organic materials are completely contacted and reacted with the reaction gas which goes from the reaction gas distribution holes to form reaction products. The design of the technology is reasonable, and the invention can be suitable for sulfonating or sulphating materials with various viscosities.
Owner:ZANYU TECH GRP CO LTD

Wet treatment method of copper smelting acid-making acid mud

The invention discloses a wet treatment method of copper smelting acid-making acid mud. The wet treatment method comprises the following steps that acid-making acid mud is pulped, a chemical agent A and a chemical agent B are added for leaching after pulping, solid-liquid separation is carried out after leaching is finished to obtain leached residues and neutral leachate, and lead, gold and silverare recovered from the leached residues; a chemical agent C is added into the obtained leachate for reduction, the final reduction potential is controlled to be 300 mV-450 mV, and solid-liquid separation is carried out to obtain mercury-rich residues and a reduced solution; the pH value of the reduced solution is controlled to be less than 1, a chemical agent D is added for reduction, solid-liquid separation is carried out after the reaction is ended to obtain crude selenium and a selenium-precipitated solution, and the selenium-precipitated solution is conveyed to a water treatment procedureto recover copper; and water is added into the mercury-rich residues for pulping, a chemical agent E is added into the solution for reaction, solid-liquid separation is carried out after the reactionis ended, after solid is separated and dried, industrial mercury is obtained, liquid can be recycled, and periodic open-circuit treatment is carried out.
Owner:HENAN ZHONGYUAN GOLD SMELTERY

Method for reducing gelation speed of konjac

ActiveCN107556496AQuality improvementViscosity maximizationAlcoholPhosphate
The invention discloses a method for reducing the gelation speed of konjac. The method comprises the following steps: firstly, adding alcohol into konjaku flour, adding a deacetylate agent, enabling the pH value to reach 7.5 to 9, carrying out a deacetylation reaction and adjusting the pH value to be neutral after reaction, and filtering and then drying filter residue; secondly, adding the powderobtained in the first step into water in a stirring state, heating to enable the powder to sufficiently swell, adding gel, uniformly mixing and enabling the pH value to reach 8.5 to 10; and finally, injecting into a mold and enabling the konjac to be subjected to gel moulding by utilizing residual temperature. By adopting the operation, the aim of reducing the gelation speed of the konjac can be achieved, compound phosphate is used as the deacetylation agent to carry out limited deacetylation modification on the konjac powder, and the deacetylation reaction of the konjac powder is mild and controllable in a low pH environment; by using compound alkali as the gel, the gelation is performed in the alkaline environment of coexistence of D-sodium erythorbate, sodium carbonate and phosphate, sothat the gelation speed is reduced, the gelation strength is not significantly affected and the gelation time is prolonged, and the gelation strength of a product is not significantly reduced.
Owner:湖北一致嘉纤生物科技有限公司

Method of preparing high-activity photocatalyst zinc magnesium composite oxide for degradation of organic dyes

The invention discloses a method of preparing a high-activity photocatalyst zinc magnesium composite oxide for degradation of organic dyes. Mg(NO3)2.6H2O and Zn(NO3) 2.6H2O are weighed and dissolved in deionized water to get a solution A. Na2CO3 is weighed and dissolved in deionized water to get a solution B. The pH values of the solutions A and B are adjusted respectively. Then a Mg (NO3)2 solution is heated, a Na2CO3 solution is quickly added to the Mg(NO3)2 solution under vigorous stirring, and stirring is continuously conducted for 2.0-6.0 min. A white precipitate is obtained after standing and ageing, and flower-like aMgCO3.bZnCO3.cMg(OH)2.dZn(OH)2.eH2O is prepared after the white precipitate is subjected to filtration, washing and drying. The flower-like aMgCO3.bZnCO3.cMg(OH)2.dZn(OH)2.eH2O is roasted in a muff furnace, and finally a high-activity spherical zinc magnesium composite oxide Mg0.8Zn0.2O catalyst with a diameter of 36 [mu]m is obtained. The invention has the advantages that the preparation method is simple, raw materials are easy to obtain, and the prepared Mg0.8Zn0.2O catalyst has high activity and a high repeated utilization ratio. Under the irradiation of ultraviolet or visible light, the prepared catalyst has higher catalytic degradation activity for organic dyes in aqueous solutions and better degradation activity for organic dyes.
Owner:XI'AN PETROLEUM UNIVERSITY

A kind of method for continuously manufacturing potassium diformate

The invention provides a method for continuously manufacturing potassium diformate. The method is characterized in that carbon dioxide gas serves as a regulating agent, formic acid and potassium hydroxide serve as raw materials, potassium diformate is synthesized in one step, and no gas is emitted in the whole reaction process. In the production process, solid potassium hydroxide is prepared into a solution, a certain quantity of the potassium hydroxide solution is obtained, and the carbon dioxide gas is introduced into the potassium hydroxide solution to prepare a potassium hydroxide and potassium carbonate mixed solution; potassium ions and formic acid with the molar ratio of 1:(2.0-3.0) are added in the mixed solution, and stirring reaction is conducted; in the reaction process, reaction temperature is kept to be 55-75 DEG C; the carbon dioxide gas generated due to reaction of formic acid and the mixed solution is recycled and reacts with a newly introduced potassium hydroxide solution; the product of the primary reaction is taken out, secondary reaction continues, reaction temperature is kept to be 55-75 DEG C, and secondary reaction lasts for 1-2.5 hours. The whole reaction is mild, controllable and free of emission, continuous production is achieved, and the method is suitable for large-scale industrial production.
Owner:BEIJING UNIV OF CHEM TECH +2

Electrochemical mineral leaching process

The invention discloses an electrochemical mineral leaching process. The electrochemical mineral leaching process comprises the following steps: (1) crushing an acid-soluble mineral to 100 to 300 meshes; (2) adding water of which the volume is 2 to 10 times the volume of the mineral to the mineral obtained in the step (1) to form slurry; (3) adding an electrolyte to the mineral slurry obtained inthe step (2); (4) inserting an anode plate and a cathode plate into the mineral slurry obtained in the step (3), and afterwards performing direct-current electrolysis for 2 to 12 hours at the voltageof 1 V to 15 V and at a current density of 1 A/m<2> to 300 A/m<2>; and (5) after electrolysis is ended, collecting elements which can be electrodeposited under an acidic condition by using the cathodeplate, and performing solid and liquid separation on the mineral slurry to obtain a material solution. According to the electrochemical mineral leaching process, salt electrolysis is used for replacing acid reaction to perform mineral leaching; the reaction is mild and controllable; the salt electrolysis effect is better than a direct acid solution effect; moreover the amount of salt-containing waste water can be greatly reduced; cyclic utilization is realized; and the electrochemical mineral leaching process disclosed by the invention is applicable to processing of various metal minerals, realizes comprehensive utilization of the minerals and is especially applicable to low-grade minerals.
Owner:四川英创环保科技有限公司

Method for continuously manufacturing potassium diformate

The invention provides a method for continuously manufacturing potassium diformate. The method is characterized in that carbon dioxide gas serves as a regulating agent, formic acid and potassium hydroxide serve as raw materials, potassium diformate is synthesized in one step, and no gas is emitted in the whole reaction process. In the production process, solid potassium hydroxide is prepared into a solution, a certain quantity of the potassium hydroxide solution is obtained, and the carbon dioxide gas is introduced into the potassium hydroxide solution to prepare a potassium hydroxide and potassium carbonate mixed solution; potassium ions and formic acid with the molar ratio of 1:(2.0-3.0) are added in the mixed solution, and stirring reaction is conducted; in the reaction process, reaction temperature is kept to be 55-75 DEG C; the carbon dioxide gas generated due to reaction of formic acid and the mixed solution is recycled and reacts with a newly introduced potassium hydroxide solution; the product of the primary reaction is taken out, secondary reaction continues, reaction temperature is kept to be 55-75 DEG C, and secondary reaction lasts for 1-2.5 hours. The whole reaction is mild, controllable and free of emission, continuous production is achieved, and the method is suitable for large-scale industrial production.
Owner:BEIJING UNIV OF CHEM TECH +2

Preparation method of graphene oxide

The invention relates to the technical field of graphene manufacturing, in particular to a preparation method of graphene oxide. The preparation method comprises the following steps: 1, mixing concentrated sulfuric acid and phosphoric acid in a mass ratio of 5: 1 to obtain mixed acid; 2, taking a certain amount of mixed acid, adding natural crystalline flake graphite powder with the mesh number of 100-5000, stirring and dispersing, and then adding potassium permanganate; 3, continuously stirring and reacting the materials in warm water at 20-60 DEG C; 4, maintaining the temperature of the mixture at 85-99 DEG C, and then adding hydrogen peroxide under a stirring condition to remove residual potassium permanganate; 5, separating the solution prepared in the step 4 by using a centrifugal machine; 6, adding a certain amount of deionized water into the precipitate obtained in the step 5, stirring and dispersing, and introducing into a homogenizer for uninterruptedly and circularly stripping; 7, separating the material obtained in the step 6 by using the centrifugal machine, and washing once by using hydrochloric acid and deionized water respectively; 8, separating the washed solids by using the centrifugal machine; the raw materials are cheap and easy to obtain, operation is safe, dispersity is good, and industrial production is facilitated.
Owner:GUANGDONG MORION NANOTECHNOLOGY CO LTD

Gas phase SO3 film-scrapping sulfonating technology

The present invention relates to a gas phase SO3 film-scraping sulfonating technology which belongs to the technical field of production technology which prepares anionic surfactant by using gas phase SO3 film-scraping sulfonating liquid organic materials. The invention is carried out according to the following steps: A: liquid SO3 is vaporized to gas phase SO3, the gas phase SO3 is sucked in a mixer shaft through a turbo-blower, the gas phase SO3 is mixed with inert gases recycled in a sulfonating reactor to reaction gas with the volume concentration being 0.1 to 10 percent, and then the reaction gas goes into a reaction cylinder body through reaction gas distribution holes on the upper part of the scraping plate shaft; B: the organic materials go into the sulfonating reactor and downwards flow along the inner wall of the reaction cylinder body, a scraping plate is rotated along with the mixer shaft under the action of a transmission system, the organic materials are continuously suffered with film scaping-spread coating-film scaping in the inner wall of the reaction cylinder body, the organic material are alternately updated and uniformly coated on the inner wall of the reaction cylinder body, and the organic materials are completely contacted and reacted with the reaction gas which goes from the reaction gas distribution holes to form reaction products. The design of the technology is reasonable, and the invention can be suitable for sulfonating or sulphating materials with various viscosities.
Owner:ZANYU TECH GRP CO LTD

Method for circularly producing nicosulfuron active compound by using byproduct phenol

The invention relates to the technical field of production of a nicosulfuron active compound, in particular to a method for circularly producing the nicosulfuron active compound by using a byproduct phenol. The method for circularly producing the nicosulfuron active compound by using the byproduct phenol comprises the following steps: reacting diphenyl carbonate with sulfonamide to generate a phenyl ester intermediate and a byproduct phenol; reacting phenyl ester with pyrimidinamine to generate nicosulfuron and a byproduct phenol; extracting and collecting phenol as a byproduct of the reaction in the two steps, and conducting reacting with solid light to obtain diphenyl carbonate; and subjecting the diphenyl carbonate obtained by the reaction to reaction with sulfonamide, and then producing phenol as a byproduct for next cyclic utilization. According to the method for circularly producing the nicosulfuron active compound by utilizing the byproduct phenol, provided by the invention, the reaction steps are mild and controllable, the process equipment is simple, the wastewater amount is small, the production cost is low, the product quality meets the requirements of high-end customers, a wastewater device of the byproduct phenol is omitted, the energy is saved, the production environment is improved, and the comprehensive utilization rate of resources is high.
Owner:ZIBO NAB AGROCHEM
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